Methods for incinerating sludge in a combustor

Abstract

A method controls mass and heat loading of sludge feed into a fluidized bed combustor (FBC) controlled via regulation of a polymer dosage or a sludge feed rate including: continuously monitoring at least one performance characteristic of the FBC; producing an input signal characteristic; analyzing the input signal and determining a first rate of change of the characteristic; generating an output signal based on the first rate of change to control addition of polymer to the FBC; generating a second output signal to control addition of sludge feed to the FBC; and determining a transition point between the addition of polymer and addition of sludge, which transition point is an upper limit of a first rate change to maintain flow so that the value of the characteristic is maintained proximate at the upper limit.

1. A method of controlling mass and heat loading of sludge feed in a fluidized bed combustor (FBC) that receives sludge and/or a polymer dosage from dewatering equipment located upstream of the FBC, the method comprising:
 continuously measuring at least one performance characteristic of the FBC and producing an input signal characteristic based on the measured at least one performance characteristic; 
 analyzing the input signal and determining a rate of change of the at least one performance characteristic; 
 determining a desired operating limit of the rate of change; 
 determining a point of transition between the addition of polymer to the dewatering equipment and the addition of sludge in order to maintain the rate of change proximate to the desired operating limit; 
 generating a first output signal based on the rate of change and the determined transition point to control addition of polymer to the dewatering equipment; and 
 generating a second output signal based on the rate of change and the determined transition point to control addition of sludge feed to the FBC. 
 
     
     
       2. The method of  claim 1 , wherein the performance characteristic is the difference between freeboard and bed temperatures ΔT. 
     
     
       3. The method of  claim 1 , further comprising regulating operation of a centrifuge to provide a selected sludge quality. 
     
     
       4. The method of  claim 1 , further comprising regulating at least one selected from the group consisting of operation a of a belt press via adjustment of belt speed or tension plate and frame press, screw press, vacuum press and a dryer to provide a selected wastewater solids quality. 
     
     
       5. The method of  claim 1 , wherein mass flow of solids to the FBC is regulated by blending influent sludge streams to control the ratio of primary and secondary sludge blends to a selected dry solids concentration based upon combustor performance. 
     
     
       6. The method of  claim 1 , further comprising a suspended solids sensor selected from the group consisting of optical, microwave, ultrasound, vibrational frequency and zeta potential sensors that detect the moisture content of the sludge prior to entering the FBC.